CN1192186C - Fossil fuel fired continuous-flow steam generator - Google Patents

Fossil fuel fired continuous-flow steam generator Download PDF

Info

Publication number
CN1192186C
CN1192186C CNB998146803A CN99814680A CN1192186C CN 1192186 C CN1192186 C CN 1192186C CN B998146803 A CNB998146803 A CN B998146803A CN 99814680 A CN99814680 A CN 99814680A CN 1192186 C CN1192186 C CN 1192186C
Authority
CN
China
Prior art keywords
steam generator
combustion chamber
type steam
conduction
generating tube
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CNB998146803A
Other languages
Chinese (zh)
Other versions
CN1330751A (en
Inventor
乔基姆·弗兰克
鲁道夫·克拉尔
埃伯哈德·威特乔
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Siemens AG
Original Assignee
Siemens AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Siemens AG filed Critical Siemens AG
Publication of CN1330751A publication Critical patent/CN1330751A/en
Application granted granted Critical
Publication of CN1192186C publication Critical patent/CN1192186C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B21/00—Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically
    • F22B21/34—Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically built-up from water tubes grouped in panel form surrounding the combustion chamber, i.e. radiation boilers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B21/00—Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically
    • F22B21/34—Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically built-up from water tubes grouped in panel form surrounding the combustion chamber, i.e. radiation boilers
    • F22B21/346—Horizontal radiation boilers

Landscapes

  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Fats And Perfumes (AREA)
  • Feeding And Controlling Fuel (AREA)

Abstract

The invention relates to a fossil fuel fired continuous-flow steam generator (2) with a gas turbine combustion chamber (4) for fossil combustibles (B). On the heating gas side a vertical gas extractor (8) is mounted downstream of the horizontal gas extractor (6). The walls (9) surrounding the combustion chamber (4) are composed of evaporator tubes (10) which are welded together and vertically arranged. The aim of the invention is to provide a continuous-flow steam generator (2) which is especially easy to produce and assemble. During operation of the continuous-flow steam generator the temperature differences between adjacent evaporator tubes (10) of the combustion chamber (4) shall be kept as low as possible. To this end, the continuous-flow steam generator (2) is provided with a number of burners (30) which are arranged in the combustion chamber (4) at the level of the horizontal gas extractor (6). Also, for a number of evaporator tubes (10) which can be simultaneously impinged by the flow medium (S) the quotient from the steam generating capacity M (indicated in kg/s) at full load and from the sum A (indicated in m<2>) of the inner cross-sectional surfaces of said evaporator tubes (10) impinged simultaneously by the flow medium (S) is less than 1350 (unit kg/sm<2>).

Description

The conduction through type steam generator that burning mineral fuel heats
The present invention relates to a kind of conduction through type steam generator, it has the combustion chamber of a burning mineral fuel, after its hot fume side is through a horizontal flue, connect a vertical gas pass, wherein the annular wall of combustion chamber by mutually weld together non-hermeticly, vertically arranged generating tube forms.
In a power station equipment that has a steam generator, utilize the fuel contained energy to make fluid media (medium) vaporization in the steam generator.Wherein fluid media (medium) transmits in vaporizer circulation usually.The steam that is made by steam generator can be used for for example driving of a steam turbine and/or the external procedure of a connection again.When steam was used to drive a steam turbine, then common turbine shaft by steam turbine made a generator or Work machine running.If the situation of generator, then the electric current of generator generation is by in feed-in one interconnected power system and/or the island formula electrical network.
Steam generator can be designed to conduction through type steam generator.By J.Franke, the paper that W.Koehler and E.Wittchow showed " the vaporization scheme of Benson steam generator " is published in VGB power station technology 73 (1993), the 4th phase, on the 352-360 page or leaf, therefrom can recognize a kind of conduction through type steam generator.In this conduction through type steam generator, the steam generator pipe that is designed to generating tube by heating is vaporized the fluid media (medium) in the steam generator pipe in disposable straight-through transmission.
Conduction through type steam generator is made the structure of vertical combustion chamber usually.This means that the medium of Combustion chamber design one-tenth confession heating or hot flue gas flow through along the direction of approximate vertical.Wherein, after the hot fume side of combustion chamber, connect a horizontal flue, make hot flue gas stream redirect to the flow direction of an approximate horizontal when carrying out the transition to horizontal flue in the combustion chamber.Yet because temperature can cause the variation of combustion chamber length usually, the combustion chamber needs a frame and hangs thereon.This causes making and very big technology input when producing conduction through type steam generator, and the structure height of conduction through type steam generator is big more, drops into just big more.Particularly all the more so under the situation of steam generating capacity greater than 80kg/s when the conduction through type steam generator full load.
The restriction if conduction through type steam generator is not stressed just can make the initial steam pressure critical pressure (P of water head and shoulders above Kri=221bar is similar to liquid and is similar between the medium of steam and have only very little density difference this moment).Higher initial steam pressure help improving the thermal efficiency and therefore reduce burning mineral fuel, for example make the CO in the power station of fuel with coal or brown coal 2Discharge capacity.
The tube wall that the there occurs-or material temperature is considered in the ring wall setting of flue or combustion chamber, is a special problem.If can guarantee that the inner surface of generating tube is moistening, to about 200bar, the temperature of combustion chamber ring wall mainly is to be determined by the height of water saturation temperature in the subcritical pressure boiler scope.This can realize by the generating tube that for example adopts side within it to have the surface structure.Especially can consider to adopt the generating tube that is added with internal-rib, its application examples in conduction through type steam generator is as being known to the public by above-mentioned document for this reason.From this so-called ribbed pipe, be that the inwall of pipeline of inner surface ribbing is good especially to the heat transmission of fluid media (medium).
Rule of thumb, the combustion chamber ring wall is differently heated inevitably.Because generating tube is subjected to different heating, the outlet temperature of the fluid media (medium) of going out from the more generating tube that is heated in the conduction through type steam generator generally will be higher than the outlet temperature of normally being heated or being heated generating tube still less.Therefore may produce the temperature difference between the adjacent generating tube, cause thermal stress, the life-span of conduction through type steam generator be reduced, even cause pipeline break.
Therefore the objective of the invention is to, the conduction through type steam generator that provides a kind of burning mineral fuel of the above-mentioned type to heat, it only needs few especially manufacturing and mounting cost, and can also make the temperature difference between the combustion chamber adjacent generating tube keep especially little in its course of work.
This purpose realizes like this according to the present invention, promptly, conduction through type steam generator has a combustion chamber that has some along the burner of horizontal flue height setting, and be designed to like this, that is, make the steam generating capacity M (in kg/s) of each generating tube some parallel connections, that can add to fluid media (medium) S simultaneously under full load and their interior cross section summation A (with m 2The meter) ratio less than 1350 (with kg/s m 2Meter).
The present invention is with that in mind: one can should have a suspended structure that can constitute with straightforward procedure with the conduction through type steam generator that few especially manufacturing and mounting cost are built.A kind of combustion chamber of building with quite few technology input hangs frame can be along with the especially little structure height of conduction through type steam generator.By the combustion chamber being made the structural shape of level, can reach the especially little purpose of conduction through type steam generator structure height.Burner is arranged on the height of the horizontal flue in the chamber wall for this reason.Therefore when conduction through type steam generator was worked, hot flue gas flow through the combustion chamber along the main flow direction of approximate horizontal.
For a horizontal firing chamber, when conduction through type steam generator is worked, see so, the heating of combustion chamber Background Region is less than heating to the combustion chamber front area in hot fume side.For example a near generating tube burner is more added heat than the one jiao of generating tube that is provided with in combustion chamber in addition.Wherein under extreme case, approximately three times of combustion chamber Background Region to the heating of combustion chamber front area.Matter current density in common now generating tube is (with kg/s m 2Meter is at 100% steam generating capacity (full load)) be 2000kg/s m 2The time, mean value with respect to the mass flow of all pipelines, the interior mass flow of the more pipeline that is heated reduces, and the mass flow in the less pipeline that is heated increases, and this characteristic is to cause owing to friction pressure loss in the total pressure of generating tube descends accounts for quite high share.The length that generating tube is relative in addition is different because the combustion chamber height is low especially, thereby is greater than the situation of vertical combustion chamber basically.This has strengthened different with friction pressure loss of being heated in single generating tube extraly.But to guarantee temperature roughly the same between the adjacent generating tube, so should design conduction through type steam generator like this: in the more generating tube that is heated, can form the higher flow of fluid media (medium) flow in the less generating tube that is heated automatically.Δ P falls in short distance (geodaetische) pressure in a generating tube that on average is heated G(in bar) is its friction pressure loss Δ P RDuring the several times of (in bar), can reach this situation usually.When mass flow was constant, the condition that mass flow increases in the more generating tube that is heated was:
( &Delta; ( &Delta;p G + &Delta;p R + &Delta;p B ) &Delta;Q ) M = cons tan i = K < 0
Δ P wherein BThe variation (in bar) that pressure falls is quickened in expression, the variation of Δ Q (in kJ/s) expression heating, and M (in kg/s) represents flow, (in (bar s)/kJ) is a constant to K.Listed condition stub in this inequality is when mass flow is constant, along with being subjected to more adding hot Δ Q, total pressure loss Δ (Δ P G+ Δ P R+ Δ P B) (in bar) minimizing, promptly one is decided to be the mathematics negative value.If identical total pressure loss as seen in some generating tubes, occurs, so according to above-mentioned inequality, be heated the certain rising of comparing in still less the generating tube of fluid media (medium) flow and in the more generating tube of being heated.
A large amount of calculating show astoundingly, if the interior cross section summation A of some of the conduction through type steam generator steam generating capacity M (in kg/s) of generating tube under full load in parallel generating tube in parallel with these is (with m 2Meter) ratio is not more than 1350 (with kg/s m 2Meter), its mathematic(al) representation is:
M/A＜1350，
The condition of the conduction through type steam generator of the listed band horizontal firing chamber of inequality just can satisfy so.
Wherein the steam generating capacity M of conduction through type steam generator under full load is also referred to as and allows production capacity for steam or the maximum continuous firing ability (BMCR) of vaporizer, and each internal cross-sectional area of generating tube refers to horizontal profile.
More advantageously, meet a public inlet accumulation-system before each generating tube of some parallel connections of combustion chamber, after meet the outlet accumulation-system of a fluid media (medium).A conduction through type steam generator that constitutes with this structure can make pressure balance between some generating tubes in parallel reliably, so all generating tubes in parallel all have identical loss of total pressure.This shows, satisfies above-mentioned inequality, and be heated a fluid media (medium) flow and in the more generating tube is heated and compares certain rising in still less the generating tube.
The generating tube of combustion chamber end wall is advantageously before the fluid media (medium) side is connected the generating tube of the ring wall that forms sidewall of combustion chamber.So just guaranteed being cooled off especially effectively of combustion chamber by the end wall of heat intensive.
In another favourable structure of the present invention, the internal diameter of the pipeline of some generating tubes of combustion chamber is selected according to residing separately position in the combustion chamber.In this manner, the generating tube in the combustion chamber can a predetermined heating profile (Beheizungsprofil) adapt with hot fume side.By consequent influence, make the temperature difference in the generating tube outlet of combustion chamber keep very little especially reliably to flowing in the generating tube.
The fluid media (medium) that is transmitted in the generating tube for the heat that makes in the combustion chamber has a good especially heat conduction, some generating tubes advantageously within it side have the rib that forms by multi start thread respectively.Wherein be preferably less than 55 ° less than 60 ° perpendicular to formed lift angle α between the side of the rib that is provided with on the plane of conduit axis and the insides of pipes.
Do not have in the generating tube that internally ribbed be heated generating tube that is so-called light pipe constitute at one, just no longer can remain and make the wetting of the especially well required certain steam content that tube wall is carried out of heat conduction.Wettingly may there be a tube wall that part is dry when not enough.Change into so dry tube wall and can cause a so-called heat to transmit crisis, its heat transfer performance worsens can make tube wall temperature sharply rise herein usually.Compare with a light pipe, this heat is transmitted crisis just in quality of steam content＞0.9 o'clock in the generating tube of a ribbing, that is to say just appearance before vaporization is about to end.This flows through the rotation that the spirality rib obtains owing to (air-flow).Because the centrifugal force difference, the water composition separates with the steam composition and is transported on the tube wall.Still can keep tube wall moistening thus when steam content is very high, making has had a high flowing velocity in the position of heat transmission crisis.Although there is heat to transmit crisis, it is comparatively good that this can make heat transmit, and the result is (obtaining) low tube wall temperature.
Some generating tubes of combustion chamber advantageously have the device that is used to reduce the fluid media (medium) flow.This designs is that throttling arrangement has confirmed it is particularly advantageous.These throttling arrangements for example can be packed in the generating tube, reduce internal diameter of the pipeline on its position in each generating tube.Also confirm simultaneously, comprise that one it is favourable in the pipe-line system of many parallel (parallel connection) pipelines the device that reduces flow being set, can be by this device to the generating tube transmission fluid media (medium) of combustion chamber.Wherein this pipe-line system can also be connected the front of a public inlet accumulation-system of generating tube some parallel connections, that can add to fluid media (medium).Wherein in many pipelines of a pipeline or system, can be provided with for example choke valve accessory.Utilize these accessories to reduce fluid media (medium) flow, can realize that the heat that adds that fluid media (medium) throughput in each root generating tube and they are subjected to separately is complementary in the combustion chamber by generating tube.Therefore the fluid media (medium) temperature difference in the generating tube exit keeps very little especially reliably.
The sidewall of horizontal flue and/or vertical gas pass advantageously by weld together airtightly mutually, the steam generator that can add to fluid media (medium) simultaneously vertically arranged, parallel with one another forms.
Adjacent vaporization or steam generator its vertical side advantageously by metal tape, be so-called fin keel mutually airtightly the welding.This fin keel can in the pipe production process, just fixedly connected with pipeline and with unit of its formation.This unit that is formed by a pipeline and fin keel is also referred to as gilled tube (Flossenrohr).The fin keel width can have influence on the heat input in generating tube or the steam generator.At this, the fin keel width is the position in conduction through type steam generator according to each vaporization or steam generator preferably, with one hot fume side can be given the heating profile suitable.This heating profile can be to heat profile by the typical case that empirical value is made, and can also be a "ball-park" estimate, for example a stairstepping heating profile.By suitably selected fin keel width, even when the heating of each vaporization or steam generator differs widely, the heat in each vaporization of input or the steam generator also can make the temperature difference at vaporization or steam generator place keep very little.In this manner, stoped the too early fatigue of material reliably.Thereby make conduction through type steam generator have long especially service life.
Advantageously be provided with some superheater surfaces in horizontal flue, they are arranged approximately perpendicular to the main flow direction of hot flue gas and it is connected in parallel for the pipeline that fluid media (medium) flows through.These with the superheater surface frame mode setting, that be also referred to as the bulkhead heating surface that hangs mainly by Convective Heating and after the fluid media (medium) side is connected the generating tube of heating clamber.Therefore guarantee to make full use of especially effectively hot flue gas heat.
Vertical gas pass preferably has some convection heating surfaces, and they are formed by the pipeline that the main flow direction approximately perpendicular to hot flue gas is provided with.These are connected in parallel for the convection heating surface pipeline that fluid media (medium) flows through.These convection heating surfaces are also mainly by Convective Heating.
Especially fully make full use of hot flue gas heat in order further to guarantee, vertical gas pass advantageously has a fuel economizer.
More advantageously, on the end wall of combustion chamber, burner is set, that is burner is set in the face of the sidewall of tap hole that leads to horizontal flue in the combustion chamber.Being designed to a such conduction through type steam generator can be complementary with the after-flame length of simple especially mode and fuel.Wherein the after-flame length of fuel is interpreted as that the hot velocity of flue gas of along continuous straight runs under certain evenly heat flue-gas temperature multiply by the tail-off time t of the flame of fuel AWherein the maximum after-flame length of each conduction through type steam generator to appear at each conduction through type steam generator full load be the operation of so-called full load, when steam generating capacity is M.The tail-off time t of fuel flame A, be again a Pulverized Coal required time of completing combustion under certain evenly heat flue-gas temperature of for example average particle size particle size.
For making material unaccounted-for (MUF) and the pollution do not expected (for example because the fusible ash content of high temperature entering) maintenance especially little, by after-flame length from combustion chamber end wall fuel when the defined combustion chamber of the distance of horizontal flue entrance area length equals the conduction through type steam generator full-load operation at least to horizontal flue.This horizontal length of combustion chamber generally be at least the combustion chamber from the bell mouth upper limb up to 80% of the height of combustion chamber top cover metering.
In order to make full use of especially the combustion heat of fossil fuel effectively, combustion chamber length L (in m) can be advantageously selected steam generating capacity M (in kg/s), the tail-off time t of fossil fuel flame during as the conduction through type steam generator full load AThe outlet temperature T of (in s) and the hot flue gas of going out from the combustion chamber BRKThe function of (in ℃).When wherein given steam generating capacity M being arranged under the conduction through type steam generator full load, the length L of combustion chamber is approximately the higher value in two functions (1) and (2):
L(M，t A)＝(C 1+C 2·M)·t A (1)
L(M，T BRK)＝(C 3·T BRK+C 4)M+C 5(T BRK) 2+C 6·T BRK+C 7 (2)
Wherein
C 1＝8m/s
C 2＝0.0057m/kg
C 3＝-1.905·10 -4(m·s)/(kg℃)
C 4＝0.286(s·m)/kg
C 5＝3·10 -4m/(℃) 2
C 6＝-0.842m/℃
C 7＝603.41m。
Here " being similar to " can be understood as and allow to have with the defined numerical value of each function+20%/-10% deviation.
The advantage that the present invention realizes mainly is: the ratio of the interior cross-sectional area summation of the steam generating capacity of some generating tubes in parallel and these generating tubes when moving by suitably selecting the conduction through type steam generator full load, can make particularly well by generating tube the fluid media (medium) flow with add heat and be complementary, and therefore guarantee that the temperature in generating tube exit is basic identical.The thermal stress in the combustion chamber ring wall that is caused by the temperature difference between the adjacent generating tube simultaneously, maintenance is well below the numerical value that risk of breakage for example takes place when conduction through type steam generator work.Therefore in a conduction through type steam generator, adopt a horizontal firing chamber also to have quite long service life.In addition, Combustion chamber design Cheng Rangre flue gas main flow direction roughly is level, also makes the structural shape of conduction through type steam generator compact especially.When this can also make conduction through type steam generator be installed in the power station that has a steam turbine, the connecting pipe from the conduction through type steam generator to the steam turbine was short especially.
By accompanying drawing one embodiment of the present of invention are described in detail below, in the accompanying drawing:
Fig. 1 is the side view of the conduction through type steam generator that heats of the burning mineral fuel of a twin flue structural shape;
Fig. 2 is the longitudinal sectional drawing of single generating tube;
Fig. 3 illustrates one and has curve K 1To K 6Coordinate system.
Corresponding components has identical Reference numeral mutually in institute's drawings attached.
Conduction through type steam generator 2 shown in Figure 1 belongs to a power station equipment that is not shown specifically, and this power station equipment also comprises a steam turbine equipment.Wherein the steam generating capacity of conduction through type steam generator when full load is decided to be 80kg/s at least.The steam that produces in the conduction through type steam generator 2 is used simultaneously in driving steam turbine, and this steam turbine itself drives a generator again and generates electricity.The electric current that generator produces is by in feed-in one interconnected power system or the island formula electrical network.
The conduction through type steam generator 2 that this burning mineral fuel heats comprises the combustion chamber 4 of a horizontal structure pattern, also is connected with a vertical gas pass 8 through a horizontal flue 6 after its hot fume side.The ring wall 9 of combustion chamber 4 by weld together airtightly mutually, vertically arranged generating tube 10 forms, fluid media (medium) S can add in the parallel generating tube of N root simultaneously.Wherein combustion chamber 4 ring wall 9 is an end wall 11.In addition, the sidewall 14 of the sidewall 12 of horizontal flue 6 or straight vertical flue 8 also can by weld together airtightly mutually, vertically arranged steam generator 16 or 17 forms.Fluid media (medium) S can add respectively in each parallel steam generator 16 or 17 simultaneously in this case.
Some generating tubes 10 in the combustion chamber 4 are connected before the outlet accumulation-system 20 after the fluid media (medium) side is connected the inlet accumulation-system 18 of fluid media (medium) S.Wherein this inlet accumulation-system 18 comprises the inlet accumulators that some are parallel.Being provided with a pipe-line system 19 simultaneously is used for directed flow body medium S and enters the inlet accumulation-system 18 of generating tube 10.This pipe-line system 19 comprises the pipeline of many parallel connections, and they link to each other with the inlet accumulators of inlet in accumulation-system 18 respectively.
Generating tube 10 (as shown in Figure 2) has an internal diameter of the pipeline D and the rib 40 on the side within it, and these ribs constitute with the multi start thread form and rib heights is R.Wherein perpendicular to the side 44 of the rib that is provided with on the plane 42 of conduit axis and the insides of pipes with the lift angle α that is become less than 55 °.The very high heat conduction of the fluid media (medium) S that is transmitted in realizing from generating tube 10 inwalls to generating tube thus makes tube wall temperature low especially simultaneously.
The internal diameter of the pipeline D of the generating tube 10 of combustion chamber 4 selectes according to generating tube 10 residing separately position in combustion chamber 4.In this manner, conduction through type steam generator 2 adapts with being heated of generating tube 10 varying strengths.The generating tube 10 of designed combustion chamber 4 can guarantee to make the temperature difference in generating tube 10 outlets to keep very little especially reliably like this.
The method that reduces fluid media (medium) S flow is that this throttling arrangement is not shown specifically in the drawings to a part of generating tube 10 installing throttling arrangements.This throttling arrangement is formed in the eyelet baffle arrangement that a certain position reduces internal diameter of the pipeline D, when conduction through type steam generator 2 work the flow of the generating tube inner fluid medium S that is heated less is reduced, and the flow of fluid media (medium) S and received heat are complementary.For reducing the flow of generating tube 10 inner fluid medium S, can also give one or more pipeline that is not shown specifically installing throttling arrangement, particularly choke valve accessory in the pipe-line system 19 in addition.
Adjacent vaporization or steam generator 10,16,17 weld together by fin keel in its longitudinal side mutually airtightly according to the mode that is not shown specifically.By suitably selecting the fin keel width will influence to the vaporization or the heating of steam generator 10,16,17.Therefore, each fin keel width and one hot fume side can be given the heating profile suitable, this heating profile depends on each vaporization or steam generator 10,16,17 position in conduction through type steam generator 2.Wherein this heating profile can be the typical heating surface of being made by empirical value, can also be a "ball-park" estimate.Therefore at each vaporization or steam generator 10,16, even the temperature difference in 17 exits also can keep very little being heated of each vaporization or steam generator 10,16,17 when differing widely.In this manner, stoped fatigue of materials reliably, thereby guaranteed that conduction through type steam generator 2 has long service life.
Need to consider for the piping of horizontal firing chamber 4: the heating of the generating tube 10 that each root is welded together mutually airtightly is very different when conduction through type steam generator 2 work.Therefore the setting of generating tube 10 will be considered that it is internally ribbed, be connected and its internal diameter of the pipeline D with the fin keel of adjacent generating tube 10, although make be heated difference but have outlet temperature about the same of whole generating tubes 10, and guarantee that under conduction through type steam generator 2 all operating modes all generating tubes 10 are sufficiently cooled off by suitable selection.Simultaneously, consider to pack into throttling arrangement extraly for the less problem of being heated of a small amount of generating tube when conduction through type steam generator 2 work.
The internal diameter of the pipeline D of the generating tube 10 in the combustion chamber 4 selectes according to generating tube 10 residing separately position in combustion chamber 4.Wherein when conduction through type steam generator 2 work by the generating tube 10 of heat intensive, its internal diameter of the pipeline D greater than when conduction through type steam generator 2 work by the generating tube 10 of mild heat.Therefore be different from the identical situation of internal diameter of the pipeline, the fluid media (medium) flows in the bigger generating tube of internal diameter of the pipeline D 10 are improved, and each generating tube 10 is reduced because of the temperature difference that is subjected to different heating and causes in its exit.Suitable for the flow and the received heat that make the fluid media (medium) S in the generating tube 10, further step is the throttling arrangement of packing in a part of generating tube 10 and/or in the pipe-line system 19 of establishing for transmission fluid media (medium) S.And suitable for the flow that makes the fluid media (medium) S that adds heat and pass through generating tube 10, the fin keel width can be selected according to the position of generating tube 10 in combustion chamber 4.Even if all these measures are heated when differing widely at each root generating tube, also can make the fluid media (medium) S that when conduction through type steam generator 2 work, transmits in the generating tube 10 that a thermal absorptivity about the same is arranged, so have only the very little temperature difference in its exit.The internally ribbed of generating tube is designed at this simultaneously: the flow of difference, conduction through type steam generator 2 fluid media (medium) S under all load conditions is also different although each root generating tube is heated, and can guarantee that also each generating tube 10 is subjected to cooling off especially reliably.
Horizontal flue 6 has some superheater surfaces 22 that are designed to bulkhead formula heating surface, and they are approximately perpendicular to the frame mode setting of main flow direction 24 to hang of hot flue gas G, and it is all in parallel for the pipeline that fluid media (medium) S flows through.Superheater surface 22 is mainly by Convective Heating, and after the fluid media (medium) side is connected the generating tube 10 of combustion chamber 4.
But vertical gas pass 8 has some mainly convection heating surfaces 26 of Convective Heating, and they are formed by the pipeline that the main flow direction 24 approximately perpendicular to hot flue gas G is provided with.These are all in parallel for the pipeline that fluid media (medium) S flows through.Also be provided with a fuel economizer 28 in this external vertical gas pass 8.Vertical gas pass 8 is passed into another heat exchanger at outlet side, for example is passed in the air preheater, and enters chimney through a dirt catcher therefrom.Being connected vertical gas pass 8 member afterwards is not shown specifically in Fig. 1.
This conduction through type steam generator 2 is designed to have the combustion chamber 4 of the low especially level of structure height, therefore only needs low especially manufacturing and mounting cost.The combustion chamber 4 of conduction through type steam generator 2 has the burner 30 of some burning mineral fuel B in addition, and they are arranged on the end wall 11 of combustion chamber 4 along the height of horizontal flue 6.
For reaching an extra high efficient, make fossil fuel B completing combustion, and preventing that hot fume side from mainly being that the superheater surface 22 of horizontal flue 6 suffers to pollute (for example harm of the fusible ash content of high temperature) and material is damaged, the length of combustion chamber 4 is selected like this: the after-flame length of fuel B when it surpasses conduction through type steam generator 2 full-load operations.Wherein this length L be from the combustion chamber 4 end wall 11 to the distance of the entrance area 32 of horizontal flue 6.Wherein the after-flame length of fuel B is defined as the tail-off time t with fuel B flames F exiting AMultiply by the speed of hot flue gas along continuous straight runs under a certain evenly heat flue-gas temperature.When the maximum after-flame length of each conduction through type steam generator 2 appears at each conduction through type steam generator 2 full-load operation.The tail-off time t of fuel B flames F exiting A, be again Pulverized Coal required time of completing combustion under a certain evenly heat flue-gas temperature of a for example average particle size particle size.
For guaranteeing to make full use of effectively especially the combustion heat of fossil fuel B, the length L of combustion chamber 4 (in m) is according to the outlet temperature T of the 4 hot flue gas G that go out from the combustion chamber BRKThe tail-off time t of (in ℃), fuel B flames F exiting ASteam generating capacity M (in kg/s) when (in s) and conduction through type steam generator 2 full load comes selected suitably.This horizontal length L of combustion chamber 4 is at least 80% of combustion chamber 4 height H simultaneously.Wherein 4 bell mouth upper limb (Fig. 1 be that the straight line of end points mark in order to X and Y) measures up to the combustion chamber top cover height H from the combustion chamber.The length L of combustion chamber 4 is determined by function (1) and (2) approx:
L(M，t A)＝(C 1+C 2·M)·t A (1)
With
L(M，T BRK)＝(C 3·T BRK+C 4)M+C 5(T BRK) 2+C 6·T BRK+C 7 (2)
Wherein
C 1＝8m/s
C 2＝0.0057m/kg
C 3＝-1.905·10 -4(m·s)/(kg℃)
C 4＝0.286(s·m)/kg
C 5＝3·10 -4m/(℃) 2
C 6＝-0.842/m/℃
C 7＝603.41m。
At this, so-called " being similar to " can be understood as and allow to have with the defined numerical value of each function+20%/-10% deviation.Wherein, when conduction through type steam generator 2 had given steam generating capacity M under full load, the higher value that is drawn by function (1) and (2) was the length L of combustion chamber 4.
As the example to the design of conduction through type steam generator 2, the pass between the steam generating capacity M the when length L of combustion chamber 4 and conduction through type steam generator 2 full load ties up in the coordinate system of Fig. 3 and is shown curve K respectively 1To K 6Wherein following each parameter corresponds respectively to these curves:
K 1: t A=3s is (1) by formula,
K 2: t A=2.5s is (1) by formula,
K 3: t A=2s is (1) by formula,
K 4: T BRK=1200 ℃ by formula (2),
K 5: T BRK=1300 ℃ by formula (2),
K 6: T BRK=1400 ℃ by formula (2).
Therefore tail-off time t for instance A=3s, and from the combustion chamber outlet temperature T of the 4 hot flue gas G that go out BRK=1200 ℃, then use curve K 1And K 4Determine the length L of combustion chamber 4.Thus, given steam generating capacity M is arranged when conduction through type steam generator 2 under full load
During M=80kg/s, press K 4Curve, length L=29m,
During M=160kg/s, press K 4Curve, length L=34m,
During M=560kg/s, press K 4Curve, length L=57m.
In above-mentioned example, always be suitable for illustrated block curve K 4
The tail-off time t of fuel B flames F exiting for instance A=2.5s, and from the combustion chamber outlet temperature T of the 4 hot flue gas G that go out BRK=1300 ℃, then use curve K 2And K 5Thus, given steam generating capacity M is arranged when conduction through type steam generator 2 under full load
During M=80kg/s, press K 2Curve, length L=21m,
During M=180kg/s, press K 2And K 5Curve, length L=23m,
During M=560kg/s, press K 5Curve, length L=37m.
As seen all be suitable for the curve K that is shown solid line up to M=180kg/s 2A part, in scope, be shown the curve K of dotted line less than this M numerical value 5Then inapplicable.For M numerical value, then be suitable for the curve K that is shown solid line greater than 180kg/s 5A part, in scope, be shown the curve K of dotted line greater than this M numerical value 2Then inapplicable.
The tail-off time t of fuel B flames F exiting for instance A=2s, and from the combustion chamber outlet temperature T of the 4 hot flue gas G that go out BRK=1400 ℃, then corresponding to curve K 3And K 6Thus, given steam generating capacity M is arranged when conduction through type steam generator 2 under full load
During M=80kg/s, press K 3Curve, length L=18m,
During M=465kg/s, press K 3And K 6Curve, length L=21m,
During M=560kg/s, press K 6Curve, length L=23m.
As seen all be suitable for the curve K that in this scope, illustrates with solid line up to M=465kg/s 3, the curve K that in this scope, illustrates with dotted line 6Inapplicable.For the M numerical value greater than 465kg/s, diagramatic curve K 6Solid line partly be suitable for diagramatic curve K 3Dotted portion inapplicable.
During conduction through type steam generator 2 work, for higher flow in the more generating tube 10 that is heated, automatically forming than the generating tube 10 that is heated still less, for the generating tube 10 of N root parallel connection, come to select the steam generating capacity M (in kg/s) of conduction through type steam generator 2 under full load like this and have internal diameter of the pipeline D respectively NThe interior cross section summation A of the generating tube 10 that can be added to simultaneously fluid media (medium) S of N root parallel connection (with m 2Meter) ratio promptly satisfies condition
M A = M &Sigma; i = 1 N &pi; ( D N 2 ) 2 < 1350
Wherein numerical value 1350 is with kg/s m 2Be unit, the internal diameter of the pipeline D of N root generating tube 10 N, i=1 to N.
When conduction through type steam generator 2 work, fossil fuel B is fed to burner 30.Wherein the flame of burner 30 points to level.Because the tectonic type of combustion chamber 4, the hot flue gas G that burning is produced is mobile along the main flow direction 24 of approximate horizontal.It arrives the roughly vertical gas pass 8 of directed towards ground through horizontal flue 6, and is discharged into the chimney direction that is not shown specifically.
The fluid media (medium) S that enters in the fuel economizer 18 enters into 18 li of the inlet accumulation-systems of conduction through type steam generator 2 combustion chambers 4 generating tubes 10 through the convection heating surfaces 26 that are provided with in the vertical gas pass 8.Vertically disposed, mutually airtightly in combustion chamber 4 generating tubes 10 of the conduction through type steam generator 2 of welding, vaporize and make the fluid media (medium) part where necessary by overheated.Wherein the steam of Chan Shenging or water-vapour-mixture accumulates in 18 li of outlet accumulation-systems of fluid media (medium) S.Steam or water-vapour-mixture enters in the superheater surface 22 of horizontal flue 6 through the sidewall of horizontal flue 6 and vertical gas pass 8 therefrom.Make steam further overheated 22 li of superheater surfaces, then carry again and go to utilize, for example be used for driving steam turbine.
By the generating tube that the N root of conduction through type steam generator 2 is parallel with one another 10 under full load steam generating capacity M and this N root generating tube in the ratio of cross section summation A be chosen to be numerical value 1350kg/s m 2, when just generating tube 10 is cooled especially reliably under guaranteeing conduction through type steam generator 2 all load conditions in simple especially mode, guarantee the especially little temperature difference between the adjacent generating tube 10.The series connection setting of generating tube 10 can make full use of the heat among the hot flue gas G that flows along the main flow direction 24 of approximate horizontal in addition.Steam generating capacity M during simultaneously according to conduction through type steam generator 2 full load selectes the length L of combustion chamber 4, makes the calory burning of fossil fuel B be able to be fully utilized especially reliably.Conduction through type steam generator 2 is because its structure height is low especially, structural shape is compact especially, so just can build up with low especially manufacturing and mounting cost in addition.Can be provided with simultaneously one with quite little technology input with regard to buildable frame.For having a steam turbine and such power station equipment with conduction through type steam generator 2 of little structure height, the connecting pipe from the conduction through type steam generator to the steam turbine can also be done shortly especially.

Claims (15)

1. a conduction through type steam generator (2), it has the combustion chamber (4) of a burning mineral fuel (B), after its hot fume side, be connected with a vertical gas pass (8) by a horizontal flue (6), wherein the ring wall (9) of combustion chamber (4) is by welding together airtightly mutually, vertically arranged generating tube (10) forms, combustion chamber (4) comprises the burner (30) that some are arranged on horizontal flue (6) height, this combustion chamber (4) is designed to like this, that is, make the interior cross section summation (A) of the many steam generating capacities (M) (in kg/s) of each generating tube (10) under full load that can be added to fluid media (medium) (S) simultaneously parallel with one another and these generating tubes (10) (with m 2The meter) ratio less than 1350 (with kg/s m 2Meter), in the combustion chamber (4) these generating tube (10) parallel with one another, that can be added to fluid media (medium) (S) simultaneously meets a public fluid media (medium) (S) inlet accumulation-system (18) respectively before fluid media (medium) one side, then connect a public outlet accumulation-system (20) in the back of these generating tubes (10), wherein, some generating tubes (10) have the rib (40) of multi start thread form within it on the side respectively.
2. according to the described conduction through type steam generator of claim 1 (2), wherein the generating tube (10) on combustion chamber (4) end wall (11) along hot flue gas flow direction be connected on other ring wall of combustion chamber (4) (9) generating tube (10) before.
3. according to claim 1 or 2 described conduction through type steam generator (2), wherein, the internal diameter of the pipeline (D) of some generating tubes (10) in the combustion chamber (4) is selected according to their residing separately positions in combustion chamber (4), makes described conduction through type steam generator (2) and being heated of described generating tube (10) varying strength adapt.
4. according to the described conduction through type steam generator of claim 3 (2), wherein perpendicular to formed lift angle (α) between the side (44) of the rib (40) that is provided with on the plane (42) of conduit axis and the insides of pipes less than 60 °.
5. according to the described once-through boiler of claim 4 (2), wherein, described lift angle (α) is less than 55 °
6. according to claim 1 or 2 described conduction through type steam generator (2), some of them generating tube (10) has a throttling arrangement respectively.
7. according to claim 1 or 2 described conduction through type steam generator (2), wherein being provided with a pipe-line system (19) is used for directed flow body medium (S) and enters in the generating tube (10) of combustion chamber (4), for reducing the flow of generating tube inner fluid medium (S), pipe-line system (19) has some throttling arrangements simultaneously.
8. according to the described conduction through type steam generator of claim 1 (2), wherein the sidewall (12) of horizontal flue (6) by weld together airtightly mutually, the steam generator (16) that can be added to fluid media (medium) (S) simultaneously vertically arranged, parallel with one another forms.
9. according to the described conduction through type steam generator of claim 1 (2), wherein, the sidewall (14) of vertical gas pass (8) by weld together airtightly mutually, the steam generator (17) that can be added to simultaneously fluid media (medium) (S) vertically arranged, parallel with one another forms.
10. according to each described conduction through type steam generator (2) in the claim 1,8 or 9, wherein, adjacent vaporization or steam generator (10,16,17) are by fin keel welding airtightly mutually, wherein the fin keel width is according to each vaporization or steam generator (10,16,17) position in combustion chamber (4), horizontal flue (6) and/or vertical gas pass (8) is selected, and making can influence vaporization or steam generator (10,16,17) heating.
11., wherein, in horizontal flue (6), be furnished with some superheater surfaces (22) with the frame mode that hangs according to claim 1 or 2 described conduction through type steam generator (2).
12., wherein, in vertical gas pass (8), be furnished with some convection heating surfaces (26) according to claim 1 or 2 described conduction through type steam generator (2).
13. according to claim 1 or 2 described conduction through type steam generator (2), wherein, burner (30) is arranged on the end wall (11) of combustion chamber (4).
14. according to claim 1 or 2 described conduction through type steam generator (2), wherein, by the after-flame length of end wall (11) fuel (B) when the length (L) of the defined combustion chamber of distance (4) of the entrance area (32) of horizontal flue (6) equals steam generator (2) full-load operation at least of (4) from the combustion chamber.
15. according to claim 1 or 2 described conduction through type steam generator (2), wherein, the steam generating capacity (M) of the length (L) of combustion chamber (4) during, the tail-off time (t of fuel (B) flame (F) as full load A) and/or the outlet temperature (T of the hot flue gas (G) that go out (4) from the combustion chamber BRK) approximation to function ground select according to array function down:
L(M，t A)＝(C 1+C 2·M)·t A (1)
With
L(M，T BRK)＝(C 3·T BRK+C 4)M+C 5(T BRK) 2+C 6·T BRK+C 7 (2)
Wherein
C 1＝8m/s
C 2＝0.0057m/kg
C 3＝-1.905·10 -4(m·s)/(kg℃)
C 4＝0.286(s·m)/kg
C 5＝3·10 -4m/(℃) 2
C 6＝-0.842m/℃
C 7＝603.41m
Wherein, when conduction through type steam generator (2) has a steam generating capacity (M) given in advance under full load, the length (L) of combustion chamber (4) is selected for use by top two higher values that function draws, wherein, and described length (L), steam generating capacity (M), completing combustion time (t A) and outlet temperature (T BRK) unit be respectively m, kg/s, s and ℃.
CNB998146803A 1998-12-18 1999-12-06 Fossil fuel fired continuous-flow steam generator Expired - Fee Related CN1192186C (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19858780.5 1998-12-18
DE19858780A DE19858780C2 (en) 1998-12-18 1998-12-18 Fossil-heated continuous steam generator

Publications (2)

Publication Number Publication Date
CN1330751A CN1330751A (en) 2002-01-09
CN1192186C true CN1192186C (en) 2005-03-09

Family

ID=7891779

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB998146803A Expired - Fee Related CN1192186C (en) 1998-12-18 1999-12-06 Fossil fuel fired continuous-flow steam generator

Country Status (12)

Country Link
US (1) US6446580B2 (en)
EP (1) EP1141625B1 (en)
JP (1) JP3571298B2 (en)
KR (1) KR100685074B1 (en)
CN (1) CN1192186C (en)
AT (1) ATE219828T1 (en)
CA (1) CA2355101C (en)
DE (2) DE19858780C2 (en)
DK (1) DK1141625T3 (en)
ES (1) ES2179696T3 (en)
RU (1) RU2212582C2 (en)
WO (1) WO2000037851A1 (en)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2501086A1 (en) * 2002-10-04 2004-04-22 Nooter/Eriksen, Inc. Once-through evaporator for a steam generator
US20050072379A1 (en) * 2003-08-15 2005-04-07 Jupiter Oxygen Corporation Device and method for boiler superheat temperature control
US7878157B2 (en) * 2004-09-23 2011-02-01 Siemens Aktiengesellschaft Fossil-fuel heated continuous steam generator
EP2065641A3 (en) * 2007-11-28 2010-06-09 Siemens Aktiengesellschaft Method for operating a continuous flow steam generator and once-through steam generator
EP2194320A1 (en) * 2008-06-12 2010-06-09 Siemens Aktiengesellschaft Method for operating a once-through steam generator and once-through steam generator
EP2182278A1 (en) * 2008-09-09 2010-05-05 Siemens Aktiengesellschaft Continuous-flow steam generator
EP2180250A1 (en) * 2008-09-09 2010-04-28 Siemens Aktiengesellschaft Continuous-flow steam generator
DE102009012321A1 (en) * 2009-03-09 2010-09-16 Siemens Aktiengesellschaft Flow evaporator
DE102010040208B4 (en) * 2010-09-03 2012-08-16 Siemens Aktiengesellschaft Solar thermal continuous evaporator heating surface with local cross-sectional constriction at its inlet
DE102013215456A1 (en) * 2013-08-06 2015-02-12 Siemens Aktiengesellschaft Through steam generator
BR112016014935B1 (en) * 2013-12-27 2022-06-14 Mitsubishi Power, Ltd HEAT TRANSFER TUBE, BOILER AND STEAM TURBINE DEVICE

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3136298A (en) * 1962-06-27 1964-06-09 Babcock & Wilcox Co Vapor generator
US3927646A (en) * 1965-04-13 1975-12-23 Babcock & Wilcox Co Vapor generator
US3527261A (en) * 1968-11-12 1970-09-08 Babcock & Wilcox Co Tube guide apparatus
DE2557427A1 (en) * 1975-12-19 1977-06-30 Kraftwerk Union Ag CIRCUIT OF A FIRE ROOM LUG IN A FLOW-THROUGH BOILER WITH GAS-TIGHT WELDED WALLS IN TWO CONSTRUCTION
US4290389A (en) * 1979-09-21 1981-09-22 Combustion Engineering, Inc. Once through sliding pressure steam generator
EP0349834B1 (en) * 1988-07-04 1996-04-17 Siemens Aktiengesellschaft Once-through steam generator
US5199384A (en) * 1988-12-22 1993-04-06 Miura Co., Ltd. Quadrangular type multi-tube once-through boiler
ATE117420T1 (en) * 1991-04-18 1995-02-15 Siemens Ag CONTINUOUS STEAM GENERATOR WITH A VERTICAL GAS CABLE MADE OF ESSENTIALLY VERTICALLY ARRANGED TUBES.
DE4427859A1 (en) * 1994-08-05 1995-10-26 Siemens Ag Tube with inner ribbing forming multi-hand thread
DE4431185A1 (en) * 1994-09-01 1996-03-07 Siemens Ag Continuous steam generator
DE19645748C1 (en) * 1996-11-06 1998-03-12 Siemens Ag Steam generator operating method
DE19651678A1 (en) * 1996-12-12 1998-06-25 Siemens Ag Steam generator
CA2334699C (en) * 1998-06-10 2008-11-18 Siemens Aktiengesellschaft Fossil-fuel-fired steam generator

Also Published As

Publication number Publication date
EP1141625A1 (en) 2001-10-10
DE59901884D1 (en) 2002-08-01
KR100685074B1 (en) 2007-02-22
RU2212582C2 (en) 2003-09-20
US6446580B2 (en) 2002-09-10
CN1330751A (en) 2002-01-09
DE19858780C2 (en) 2001-07-05
JP3571298B2 (en) 2004-09-29
DK1141625T3 (en) 2002-10-14
KR20010082364A (en) 2001-08-29
CA2355101C (en) 2005-07-26
JP2002533643A (en) 2002-10-08
ES2179696T3 (en) 2003-01-16
EP1141625B1 (en) 2002-06-26
DE19858780A1 (en) 2000-07-06
ATE219828T1 (en) 2002-07-15
WO2000037851A1 (en) 2000-06-29
CA2355101A1 (en) 2000-06-29
US20020000208A1 (en) 2002-01-03

Similar Documents

Publication Publication Date Title
CN1192186C (en) Fossil fuel fired continuous-flow steam generator
CN1192185C (en) Fossil fuel fired steam generator
US20110083619A1 (en) Dual enhanced tube for vapor generator
CN1265865C (en) CFB impact dust collecting device fixed on cooling bearing pipe
CN1126904C (en) Fossil-fuel heated steam generator, comprising denitrification device for heating gas
CN103940248A (en) Heat accumulation type electric furnace flue gas waste heat recovery system
CN108775573A (en) A kind of novel electricity generation boiler of burning away the refuse
CN1192189C (en) Fossil-fuel fired continuous steam type boiler
CN103363517B (en) A kind of high bed temperature CFBB of 700 DEG C and above steam parameter
CN1193191C (en) Fossil-fuel fired continuous-flow steam cenerator
CN1192187C (en) Fossil fuel fired steam generator
CN1192188C (en) Fossil fuel fired steam generator
KR101354938B1 (en) Fluidized bed combustor
CN208670988U (en) A kind of novel electricity generation boiler of burning away the refuse
CN103759239B (en) Detachable steam generator
JP2023539769A (en) steam generator
CN219510762U (en) Tubular steam generator
CN203731362U (en) Detachable vapor generator
CN218469056U (en) Modular steam generator system with through-flow straight water pipe
KR20130113350A (en) Apparatus for connecting an insert in a steam generator tube with a material bond, comprising a welding wire nozzle arranged eccentrically with respect to the centre axis of the torch tube
CN116123520A (en) Tubular steam generator
RU2194925C2 (en) Vertical hot-water boiler
CN111853748A (en) Horizontal combined fuel oil and gas biomass steam generator
US6067944A (en) Furnace floor
CN114607992A (en) Heterogeneous tube bundle group heat exchange structure, corner tube boiler and operation method of corner tube boiler

Legal Events

Date Code Title Description
C06 Publication
C10 Entry into substantive examination
PB01 Publication
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20050309

Termination date: 20161206

CF01 Termination of patent right due to non-payment of annual fee